Mixture of Disiloxane, hexamethyl- + Heptane
Datasets
-
Excess molar enthalpy (molar enthalpy (6)
-
Excess molar volume, m3/mol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Disiloxane, hexamethyl- (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.5000 |
298.15 |
101.00 |
5.0 |
Partial molar enthalpy, kJ/mol of Disiloxane, hexamethyl- (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Partial molar enthalpy, kJ/mol of Disiloxane, hexamethyl- (1) - Liquid |
0.4837 |
0.1519 |
0.4877 |
0.1560 |
0.4917 |
0.1592 |
0.4959 |
0.1613 |
0.5001 |
0.1655 |
0.5043 |
0.1687 |
0.5087 |
0.1708 |
0.5131 |
0.1710 |
0.7299 |
0.3812 |
0.7353 |
0.3863 |
0.7407 |
0.3945 |
0.7461 |
0.3996 |
0.7472 |
0.4049 |
0.7517 |
0.4068 |
0.7518 |
0.4110 |
0.7573 |
0.4130 |
0.7613 |
0.4153 |
0.7630 |
0.4222 |
0.7689 |
0.4253 |
0.7710 |
0.4235 |
0.7760 |
0.4287 |
0.8207 |
0.4897 |
0.8252 |
0.4958 |
0.8297 |
0.5009 |
0.8436 |
0.5244 |
0.8484 |
0.5315 |
0.8532 |
0.5396 |
0.8631 |
0.5613 |
0.8679 |
0.5651 |
0.8691 |
0.5705 |
0.8729 |
0.5662 |
0.8751 |
0.5777 |
0.8780 |
0.5754 |
0.8812 |
0.5889 |
0.8874 |
0.5981 |
0.8937 |
0.6073 |
0.9001 |
0.6185 |
0.9065 |
0.6287 |
0.9131 |
0.6380 |
0.9265 |
0.6744 |
0.9334 |
0.6856 |
0.9342 |
0.6729 |
0.9390 |
0.6791 |
0.9403 |
0.6999 |
0.9439 |
0.6882 |
0.9474 |
0.7091 |
0.9539 |
0.7096 |
0.9546 |
0.7233 |
0.9589 |
0.7207 |
0.9619 |
0.7375 |
0.9640 |
0.7269 |
0.9692 |
0.7381 |
0.9693 |
0.7528 |
0.9768 |
0.7650 |
0.9844 |
0.7833 |
0.9904 |
0.7755 |
0.9921 |
0.7995 |
0.9931 |
0.7806 |
Partial molar enthalpy, kJ/mol of Heptane (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Partial molar enthalpy, kJ/mol of Heptane (2) - Liquid |
0.0318 |
0.5928 |
0.0470 |
0.5777 |
0.0616 |
0.5637 |
0.0759 |
0.5495 |
0.0897 |
0.5344 |
0.1031 |
0.5202 |
0.1161 |
0.5089 |
0.1288 |
0.4917 |
0.1647 |
0.4647 |
0.1760 |
0.4553 |
0.1870 |
0.4449 |
0.1977 |
0.4344 |
0.2081 |
0.4250 |
0.2183 |
0.4075 |
0.2282 |
0.4040 |
0.2379 |
0.3985 |
0.2473 |
0.3899 |
0.2565 |
0.3804 |
0.2655 |
0.3748 |
0.2742 |
0.3662 |
0.2828 |
0.3586 |
0.4957 |
0.1912 |
0.5015 |
0.1895 |
0.5071 |
0.1868 |
0.5126 |
0.1840 |
0.5180 |
0.1802 |
0.5233 |
0.1765 |
0.5285 |
0.1747 |
0.7355 |
0.0622 |
0.7382 |
0.0613 |
0.7408 |
0.0594 |
0.7434 |
0.0585 |
0.7459 |
0.0576 |
0.7484 |
0.0567 |
0.7509 |
0.0558 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Disiloxane, hexamethyl- (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.5000 |
298.15 |
101.00 |
5.0 |
Partial molar enthalpy, kJ/mol of Disiloxane, hexamethyl- (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Partial molar enthalpy, kJ/mol of Disiloxane, hexamethyl- (1) - Liquid |
0.4837 |
0.1519 |
0.4877 |
0.1560 |
0.4917 |
0.1592 |
0.4959 |
0.1613 |
0.5001 |
0.1655 |
0.5043 |
0.1687 |
0.5087 |
0.1708 |
0.5131 |
0.1710 |
0.7299 |
0.3812 |
0.7353 |
0.3863 |
0.7407 |
0.3945 |
0.7461 |
0.3996 |
0.7472 |
0.4049 |
0.7517 |
0.4068 |
0.7518 |
0.4110 |
0.7573 |
0.4130 |
0.7613 |
0.4153 |
0.7630 |
0.4222 |
0.7689 |
0.4253 |
0.7710 |
0.4235 |
0.7760 |
0.4287 |
0.8207 |
0.4897 |
0.8252 |
0.4958 |
0.8297 |
0.5009 |
0.8436 |
0.5244 |
0.8484 |
0.5315 |
0.8532 |
0.5396 |
0.8631 |
0.5613 |
0.8679 |
0.5651 |
0.8691 |
0.5705 |
0.8729 |
0.5662 |
0.8751 |
0.5777 |
0.8780 |
0.5754 |
0.8812 |
0.5889 |
0.8874 |
0.5981 |
0.8937 |
0.6073 |
0.9001 |
0.6185 |
0.9065 |
0.6287 |
0.9131 |
0.6380 |
0.9265 |
0.6744 |
0.9334 |
0.6856 |
0.9342 |
0.6729 |
0.9390 |
0.6791 |
0.9403 |
0.6999 |
0.9439 |
0.6882 |
0.9474 |
0.7091 |
0.9539 |
0.7096 |
0.9546 |
0.7233 |
0.9589 |
0.7207 |
0.9619 |
0.7375 |
0.9640 |
0.7269 |
0.9692 |
0.7381 |
0.9693 |
0.7528 |
0.9768 |
0.7650 |
0.9844 |
0.7833 |
0.9904 |
0.7755 |
0.9921 |
0.7995 |
0.9931 |
0.7806 |
Partial molar enthalpy, kJ/mol of Heptane (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Partial molar enthalpy, kJ/mol of Heptane (2) - Liquid |
0.0318 |
0.5928 |
0.0470 |
0.5777 |
0.0616 |
0.5637 |
0.0759 |
0.5495 |
0.0897 |
0.5344 |
0.1031 |
0.5202 |
0.1161 |
0.5089 |
0.1288 |
0.4917 |
0.1647 |
0.4647 |
0.1760 |
0.4553 |
0.1870 |
0.4449 |
0.1977 |
0.4344 |
0.2081 |
0.4250 |
0.2183 |
0.4075 |
0.2282 |
0.4040 |
0.2379 |
0.3985 |
0.2473 |
0.3899 |
0.2565 |
0.3804 |
0.2655 |
0.3748 |
0.2742 |
0.3662 |
0.2828 |
0.3586 |
0.4957 |
0.1912 |
0.5015 |
0.1895 |
0.5071 |
0.1868 |
0.5126 |
0.1840 |
0.5180 |
0.1802 |
0.5233 |
0.1765 |
0.5285 |
0.1747 |
0.7355 |
0.0622 |
0.7382 |
0.0613 |
0.7408 |
0.0594 |
0.7434 |
0.0585 |
0.7459 |
0.0576 |
0.7484 |
0.0567 |
0.7509 |
0.0558 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0541 |
-2.5000e-08 |
0.0752 |
-3.4000e-08 |
0.1111 |
-4.0000e-08 |
0.1978 |
-6.9000e-08 |
0.1982 |
-6.5000e-08 |
0.2921 |
-8.2000e-08 |
0.3131 |
-8.8000e-08 |
0.3968 |
-9.1000e-08 |
0.4121 |
-9.9000e-08 |
0.4936 |
-9.5000e-08 |
0.4957 |
-1.0200e-07 |
0.5892 |
-9.8000e-08 |
0.6792 |
-9.6000e-08 |
0.7073 |
-9.2000e-08 |
0.7762 |
-8.0000e-08 |
0.8013 |
-6.4000e-08 |
0.8729 |
-4.9000e-08 |
0.8956 |
-3.7000e-08 |
0.9237 |
-3.0000e-08 |
0.9528 |
-1.9000e-08 |
0.9606 |
-1.5000e-08 |
0.9737 |
-1.0000e-08 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0541 |
-2.5000e-08 |
0.0752 |
-3.4000e-08 |
0.1111 |
-4.0000e-08 |
0.1978 |
-6.9000e-08 |
0.1982 |
-6.5000e-08 |
0.2921 |
-8.2000e-08 |
0.3131 |
-8.8000e-08 |
0.3968 |
-9.1000e-08 |
0.4121 |
-9.9000e-08 |
0.4936 |
-9.5000e-08 |
0.4957 |
-1.0200e-07 |
0.5892 |
-9.8000e-08 |
0.6792 |
-9.6000e-08 |
0.7073 |
-9.2000e-08 |
0.7762 |
-8.0000e-08 |
0.8013 |
-6.4000e-08 |
0.8729 |
-4.9000e-08 |
0.8956 |
-3.7000e-08 |
0.9237 |
-3.0000e-08 |
0.9528 |
-1.9000e-08 |
0.9606 |
-1.5000e-08 |
0.9737 |
-1.0000e-08 |
Sources